Strategy for choosing the optimum design of reactor units in chemical engineering networks
Viatcheslav Kafarov, А.А. Reznichenko, V. A. Ivanov
Abstract
Viatcheslav Kafarov, А.А. Reznichenko, V. A. Ivanov
Abstract
A procedure has been developed for selecting the structural design of chemical reactors based on a three-level optimization algorithm that employs an effective cost criterion. The maximum reactor productivity is calculated under conditions in which an optimum temperature profile is realized in the catalyst bed. Results are given for the optimization of the design parameters of multiple-tray catalytic reactors for the joint synthesis of methanol and higher alcohols.
A significance statement is not available in the OpenAlex record.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
A procedure has been developed for selecting the structural design of chemical reactors based on a three-level optimization algorithm that employs an effective cost criterion. The maximum reactor productivity is calculated under conditions in which an optimum temperature profile is realized in the catalyst bed. Results are given for the optimization of the design parameters of multiple-tray catalytic reactors for the joint synthesis of methanol and higher alcohols.
Key concepts: Process engineering, Chemical reactor, Methanol, Reactor design, Tray, Catalysis, Chemical reaction engineering, Engineering